HCBBS Forum (English)
Submit Chemical Projects / Find Solutions
Amplify Your Requirements on a Broader Chemical Platform *Engineering · Technology · Equipment · Solutions*
Submit Request

On EDR simulated thermosiphon reboilers

2017-02-19View Original

Thread Content

When using EDR to simulate a thermal siphon reboiler, how should the pipe length term be calculated in the pipeline pressure loss calculation? Does it refer only to the length of the straight pipe section, or does it also include the length of fittings such as elbows (from the center of the elbow to its end)? For large pipes, the difference between the two is significant. Please give me some advice!
Reply #22017-02-21
If I remember correctly, there is a siphon type in EDR, where you are required to enter details such as the exact length, the number of elbows, and the type of elbows
Reply #32023-12-12
As I recall, the pipes in thermal siphons don’t have valves; there are only bends, tees, and things like that
Reply #42023-12-13
With a valve added, it’s highly likely that thermal siphonning will no longer occur; the pressure drop that thermal siphonning overcomes is already very small, and by installing a valve and setting a certain opening degree, circulation may cease

Submit a Project

**Looking for Chemical Technology, Equipment & Solutions?** No Registration Required Broader Platform Exposure | Global Chemical Service Provider Connections

Submit Request — Free Consultation

Disclaimer

This is an automated machine translation of the original thread. Some technical terms may have inaccuracies; the original text shall prevail. Click "View Original" at the top right to access the source page, which supports IP-based automatic real-time language translation. Please watch out for contact details and sales inducements to prevent fraud. All content and translations are for reference only, representing solely the poster's personal views. For enquiries, email service@hcbbs.com.